Forma+de+Calcular+El+Recalentamiento

July 10, 2019 | Author: Santiago Humberto Chau Velásquez | Category: Ingeniería de construcción, Termodinámica atmosférica, Química física, Ramas de la termodinámica, Química
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TABLA TEMPERATURA - PRESION

 ® 

°C

REFRIGERANTE - psig

°F 12 (F)

-50 -4 8 -46 -4 4 -42 -4 0 -38 -3 6 -34 -3 2 -30 -2 8 -26 -2 4 -22 -2 0 -19 -1 8 -17 -1 6 -15 -1 4 -13 -1 2 -11 -1 0 -9 -8 -7 -6 -5 -4 -3 -2 -1 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 52 54 56 58 60 62 64 66 68 70 72 74

-58.0 -54.4 -50.8 -47.2 -43.6 -40.0 -36.4 -32.8 -29.2 -25.6 -22.0 -18.4 -14.8 -11.2 -7.6 -4.0 -2.2 -0.4 1.4 3.2 5.0 6.8 8.6 10.4 12.2 14.0 15.8 17.6 19.4 21.2 23.0 24.8 26.6 28.4 30.2 32.0 33.8 35.6 37.4 39.2 41.0 42.8 44.6 46.4 48.2 50.0 51.8 53.6 55.4 57.2 59.0 60.8 62.6 64.4 66.2 68.0 69.8 71.6 73.4 75.2 77.0 78.8 80.6 82.4 84.2 86.0 87.8 89.6 91.4 93.2 95.0 96.8 98.6 100.4 102.2 104.0 105.8 107.6 109.4 111.2 113.0 114.8 116.6 118.4 120.2 122.0 125.6 129.2 132.8 136.4 140.0 143.6 147.2 150.8 154.4 158.0 161.6 165.2

22 (V)

134a (J)

502 (R)

507 (P)

404A (S) 407C (N)

18 .4 

10 .9 

21.1

5.9 

4.5 

5.5 

15 .1

17 .1

8.8 

20 .0 

3.4 

1.8 

3.0 

13 .4 

15 .8 

6.6 

18 .9 

0 .8 

0.2 

11.5 

14 .3 

4.2 

17 .6 

1.6 

16 .2 

11.0 

0.6 2.0 3.6 5.3 7.1 9.1 11.1 13.4 15.7 18.2 20.9 22.3 23.7 25.2 26.7 28.3 29.9 31.5 33.2 35.0 36.8 38.6 40.5 42.5 44.4 46.5 48.6 50.8 53.0 55.2 57.5 59.9 62.4 64.9 67.4 70.0 72.7 75.5 78.3 81.2 84.1 87.1 90.2 93.3 96.5 99.8 103.2 106.6 110.1 113.7 117.3 121.1 124.9 128.8 132.7 136.8 140.9 145.1 149.4 153.8 158.2 162.8 167.4 172.1 177.0 181.9 186.9 192.0 197.1 202.4 207.8 213.3 218.9 224.5 230.3 236.2 242.2 248.3 254.5 260.8 267.2 280.3 293.9 307.9 322.5 337.5 353.0 369.0 385.5 402.5 420.1 438.2 456.9

14 .7 

1.3 2.9 4.6 6.4 8.3 10.4 12.6 15.0 17.5 20.1 23.0 26.0 29.2 30.9 32.6 34.3 36.2 38.0 39.9 41.9 43.9 46.0 48.1 50.3 52.6 54.9 57.3 59.7 62.2 64.7 67.3 70.0 72.7 75.5 78.4 81.4 84.4 87.4 90.6 93.8 97.1 100.5

9 .5 

12 .7 

1.0 2.5 4.1 5.8 7.7 9.7 11.8 14.0 16.4 18.9 21.6 24.5 27.5 29.1 30.7 32.4 34.1 35.9 37.7 39.5 41.4 43.4 45.4 47.5 49.6 51.7 53.9 56.2 58.5 60.9 63.4 65.9 68.4 71.0 73.7 76.5 79.3 82.1 85.1 88.1 91.1 94.2 97.4 100.7 104.0 107.4 110.9 114.4 118.0 121.7 125.5 129.3 133.2 137.2 141.2 145.4 149.6 153.9 158.3 162.7 167.3 171.9 176.6 181.4 186.3 191.2 196.3 201.4 206.7 212.0 217.4 222.9 228.5 234.2 240.0 245.9 251.9 258.0 264.2 270.5 276.9 283.4 290.1 303.6 317.7 332.2 347.1 362.6 378.6 395.1 412.2 429.9 448.2 467.2 486.9

0.5 2.1 3.7 5.5 7.4 9.4 11.6 13.9 16.4 19.0 21.8 24.8 28.0 31.3 33.0 34.8 36.7 38.5 40.5 42.5 44.5 46.6 48.8 51.0 53.3 55.6 58.0 60.4 62.9 65.5 68.1 70.8 73.6 76.4 79.3 82.3 85.3 88.4 91.6 94.8 98.1 101.5 105.0 108.6 112.2 115.9 119.7 123.6 127.5 131.6 135.7 139.9 144.2 148.6 153.1 157.7 162.3 167.1 172.0 176.9 182.0 187.2 192.5 197.8 203.3 208.9 214.6 220.5 226.4 232.5 238.6 244.9 251.4 257.9 264.6 271.4 278.3 285.4 292.6 299.9 307.4 315.0 322.8 330.7 347.0 364.0 381.5 399.8 418.7 438.4 458.8 480.1 502.1 524.9 ** **

9 .1 7 .2  5 .0  2 .7  0 .3 

1.1 2.5 4.0 5.5 7.2 8.0 8.9 9.8 10.8 11.8 12.8 13.8 14.8 15.9 17.0 18.2 19.4 20.6 21.8 23.1 24.4 25.8 27.1 28.6 30.0 31.5 33.0 34.6 36.2 37.8 39.5 41.2 43.0 44.8 46.6 48.5 50.4 52.4 54.4 56.5 58.6 60.7 62.9 65.2 67.5 69.8 72.2 74.6 77.1 79.7 82.3 84.9 87.6 90.4 93.2 96.0 98.9 101.9 104.9 108.0 111.2 114.4 117.7 121.0 124.4 127.8 131.3 134.9 138.5 142.2 146.0 149.8 153.7 157.7 161.7 170.0 178.6 187.4 196.6 206.0 215.7 225.8 236.2 246.9 257.9 269.3 281.0

13 .0  11.2  9 .3  7 .2  4 .9  2 .4 

0.1 1.5 3.0 4.6 5.4 6.3 7.2 8.1 9.1 10.1 11.1 12.2 13.3 14.4 15.6 16.8 18.0 19.3 20.6 22.0 23.4 24.8 26.3 27.8 29.3 30.9 32.6 34.3 36.0 37.8 39.6 41.5 43.4 45.4 47.5 49.5 51.7 53.9 56.1 58.4 60.8 63.2 65.7 68.2 70.8 73.5 76.2 78.9 81.8 84.7 87.7 90.7 93.8 97.0 100.2 103.6 106.9 110.4 113.9 117.5 121.2 125.0 128.8 132.7 136.7 140.8 144.9 149.2 153.5 157.9 162.4 167.0 171.7 176.4 186.2 196.4 206.9 217.8 229.2 240.9 253.1 265.7 278.7 292.2 306.2 320.7

105.5 109.1        A        J112.7        U 116.4        B        R 120.2        U        B 124.1        E128.0        D 132.1        O        T136.2        N 140.4        U        P 144.7 149.1 153.5 158.1 162.8 167.5 172.3 177.3 182.3 187.4 192.7 198.0 203.4 209.0 214.6 220.4 226.2 232.2 238.3 244.4 250.7 257.2 263.7 270.3 277.1 284.0 291.0 298.1 305.3 312.7 320.2 335.6 351.5 368.0 385.0 402.6 420.8 439.5 458.9 479.4 500.8 523.2 **

7 .2  4 .8  2 .2 

0.3 1.8 3.4 5.2 7.0 9.0 11.2 13.5 15.9 17.2 18.6 19.9 21.4 22.8 24.3 25.9 27.5 29.1 30.9 32.6 34.4 36.3 38.2 40.2 42.2 44.3 46.4 48.6 50.9 53.2 55.6 58.0 60.5 63.1 65.8 68.5 71.3 74.1

96.4        A99.8        J103.3        U 106.8        B        R 110.4        U        B 114.1        E117.9        D 121.7        O        T125.7        N 129.7        U        P 133.8 138.0 142.3 146.6 151.1 155.7 160.3 165.0 169.9 174.8 179.8 184.9 190.2 195.5 200.9 206.4 212.0 217.8 223.6 229.5 235.6 241.7 248.0 254.4 260.9 267.5 274.2 281.0 288.0 295.0 302.2 317.0 332.2 347.9 364.2 380.9 398.2 416.1 434.5 453.4 472.9 493.1 513.7

** Excede la temperatura crítica. PRESION - Libras por pulgada cuadrada VACIO - Pulgadas de mercurio - letras itálicas DIAGRAMA P-H PARA MEZCLAS Cycle de Refrigeration

Punto De Burbuja

Lineas de Temperatura constante

Punto de Rocío

Para determinar el subenfriamiento en las mezclas de refrigerantes usa el punto (líquido) de Burbuja (valores en Azul) Para determinar el recalentamiento en las mezclas de refrigerantes usa el punto (vapor) de rocío (valores en Negro) Sporlan Division Parker Hannifin Corporation 206 Lange Drive

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